IP Library Patent Application 11884018
Patent Application
App. No. 11/884,018

Method For the Optimalization of the Supply of Chemicals

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Quick Facts
Patent No.
US None
App. No.
11/884,018
Abstract

A method for optimising the use of chemicals, in particular the use of antifoaming agents and emulsion breakers, for gas/oil/water fluid in oil processing plants on the seabed, onshore or offshore. The chemicals are dosed on the basis of the effect they have on the thickness of the foam layer and the emulsion layer, respectively, of the fluid. The fluid may expediently be supplied to and separated in a separator ( 1 ); the measurement of the emulsion and foam layers is performed by a measuring device ( 3 ), which emits signals to a control device ( 4 ), which controls the operation of pumps ( 5, 6 ), which, in turn, pump, at all times, the measured quantity of chemical to the fluid to be separated.

Claims (30)

1 . A method for optimising the use of chemicals, in particular the use of antifoaming agents and emulsion breakers, for gas/oil/water fluid in oil processing plants on the seabed, onshore or offshore.

characterised in that

the chemicals are dosed on the basis of the effect they have on the thickness of the foam layer and the emulsion layer, respectively, of the fluid.

2 . A method in accordance with claim 1 ,

characterised in that

the chemicals are an antifoaming agent and/or an emulsion breaker.

3 . A method in accordance with claim 1 , in which the fluid is supplied, via a supply line ( 2 ), to a separator ( 1 ) and is separated in the separator ( 1 ),

characterised in that

the measurement of the emulsion and foam layers is performed by a measuring device ( 3 ), which emits signals to a control device ( 4 ), which controls the operation of pumps ( 5 , 6 ), which, in turn, pump, at all times, the measured quantity of chemical to the fluid to be separated.

4 . A method in accordance with claim 3 ,

characterised in that

the chemicals are added in the supply line ( 2 ).

5 . A method in accordance with claim 3 ,

characterised in that

a water-cut meter ( 11 ) on the outlet line ( 14 ) measures the water quantity in the separated oil phase and an oil-in-water meter ( 12 ) on the outlet line ( 15 ) measures the oil concentration in the separated water phase flowing from the separator ( 1 ); these measurements are used in the adjustment algorithms in the control device ( 4 ) to improve the precision of the control method.

6 . A method in accordance with claim 2 , in which the fluid is supplied, via a supply line ( 2 ), to a separator ( 1 ) and is separated in the separator ( 1 ),

characterised in that

the measurement of the emulsion and foam layers is performed by a measuring device ( 3 ), which emits signals to a control device ( 4 ), which controls the operation of pumps ( 5 , 6 ), which, in turn, pump, at all times, the measured quantity of chemical to the fluid to be separated.

7 . A method in accordance with claim 6 ,

characterised in that

the chemicals are added in the supply line ( 2 ).

8 . A method in accordance with claim 4 ,

characterised in that

a water-cut meter ( 11 ) on the outlet line ( 14 ) measures the water quantity in the separated oil phase and an oil-in-water meter ( 12 ) on the outlet line ( 15 ) measures the oil concentration in the separated water phase flowing from the separator ( 1 ); these measurements are used in the adjustment algorithms in the control device ( 4 ) to improve the precision of the control method.

9 . A method in accordance with claim 6 ,

characterised in that

a water-cut meter ( 11 ) on the outlet line ( 14 ) measures the water quantity in the separated oil phase and an oil-in-water meter ( 12 ) on the outlet line ( 15 ) measures the oil concentration in the separated water phase flowing from the separator ( 1 ); these measurements are used in the adjustment algorithms in the control device ( 4 ) to improve the precision of the control method.

10 . A method in accordance with claim 7 ,

characterised in that

a water-cut meter ( 11 ) on the outlet line ( 14 ) measures the water quantity in the separated oil phase and an oil-in-water meter ( 12 ) on the outlet line ( 15 ) measures the oil concentration in the separated water phase flowing from the separator ( 1 ); these measurements are used in the adjustment algorithms in the control device ( 4 ) to improve the precision of the control method.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 13, 2013
From: STATOIL ASA
To: STATOIL PETROLEUM AS
Reel/Frame 031627/0265 →
CHANGE OF NAME Recorded Oct 31, 2013
From: STATOILHYDRO ASA
To: STATOIL ASA
Reel/Frame 031528/0807 →
CHANGE OF NAME Recorded Oct 25, 2013
From: STATOIL ASA
To: STATOILHYDRO ASA
Reel/Frame 031495/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 14, 2007
From: GRAMME, PER EIVIND; LIE, GUNNAR HANNIBAL
To: NORSK HYDRO ASA
Reel/Frame 019923/0583 →